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Test Re,)o <br />Calculations (Water Only) <br />EWO NO. AFE 11 <br />REPORT NO. <br />i�� CNEIh�'ac Go�tr DATE �o/1o/d7 <br />CLIENT <br />PROJECT NAME r <br />ll <br />CONTRACTOR (S) u!'S• h /kC. <br />TEST. SECTION DESCRIPT <br />PIPE DIAMETER <br />PIPE GRADE <br />STD. MILL TEST PRESS. _ <br />HYDROSTATIC TEST PRE <br />MINIMILIMTEST PRESSUP <br />UNIT VOLUME AT 60�F <br />NET VOLUME ADDED TC <br />DATE OF TEST <br />TIME OF TEST <br />TEST PRESSURE <br />TEMPERATURE ��Ra <br />Fwrp <br />Fpp <br />Fp n <br />(VOLUME AT TEST <br />6 vtpw <br />UNACCOUNTABLE D <br />FLUID LOSS RATE <br />TEST ACCEPTED <br />NOTES: <br />'Vtp = Vo (Fwp) (Ft <br />APOSITIVE DEVIL <br />ERROR <br />A NEGATIVE DEV <br />VALUES_BETWEEI <br />.._I <br />/0. ?SO inch <br />NOMINAL WALL THICKNESS inch <br />SECTION LENGTH <br />/55, 740 feet 2f 5 k <br />psq <br />PRESSURE TO YEILC <br />/2Z4= Pik <br />,, psl9 <br />MIN. ALLOWABLE PRESS.... <br />I RING TEST PERIOD <br />aco <br />psq <br />D <br />¢,• 3�i ofo pal/h <br />TOTAL YO LUME W.)C�3 <br />>g 7T • 4 GL <br />+) OR BLED FROM (-) TEST SECTION (Vm) <br />R _ <br />I! <br />(2) <br />INITIAL <br />FINAL' <br />d <br />io/i5 497 <br />I <br />psg <br />I 1 oo= ...: - . psro <br />-78 .F <br />CtIAaT) <br />QV3Q7 ,w <br />/. G�0547G. 4�j4 <br />/ A�S`354810 <br />� <br />0. 91"2 9 2 00 <br />p.948Zc� 'TCaO <br />'' <br />loci •732�'S ¢al. <br />Coft 7I7.8 �I• <br />' E <br />p & PRESS ? <br />. <br />I <br />/4•► 7 2 <br />gal. <br />0)f Vtp(2f VrrA 1 <br />tP <br />x 100% a• 002 <br />% (SEE NOTES) <br />(6v <br />ION <br />; <br />Nt.* <br />PRESSURE LOSS RATE <br />~tA <br />TEST ENGINEER. <br />I GLIEN•F xmw <br />r E <br />OF <br />s tit <br />C <br />11 (Fwpt) * . <br />Jr <br />1 ION REPRESENTS FLUID GAIN AND IS DUE TO MEASUREMENT ' unq <br />►TION REPRESENTS FLUID LOSS AND IS ACCEPTABLE FOR. <br />0.00% and <br />I, , <br />